EP0219473A1 - Procédé de récupération sélective du plomb à partir de minearais complexes sulfurés de métaux non ferreux - Google Patents
Procédé de récupération sélective du plomb à partir de minearais complexes sulfurés de métaux non ferreux Download PDFInfo
- Publication number
- EP0219473A1 EP0219473A1 EP86850290A EP86850290A EP0219473A1 EP 0219473 A1 EP0219473 A1 EP 0219473A1 EP 86850290 A EP86850290 A EP 86850290A EP 86850290 A EP86850290 A EP 86850290A EP 0219473 A1 EP0219473 A1 EP 0219473A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- lead
- concentrate
- electrolytic cell
- electrolyte
- cell
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 27
- 239000012141 concentrate Substances 0.000 title claims abstract description 23
- 239000002184 metal Substances 0.000 title claims abstract description 7
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 7
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 title claims abstract description 4
- 239000000725 suspension Substances 0.000 claims abstract description 21
- 239000003792 electrolyte Substances 0.000 claims abstract description 17
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims abstract description 6
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000005864 Sulphur Substances 0.000 claims abstract description 4
- 238000005363 electrowinning Methods 0.000 claims abstract description 4
- 238000009835 boiling Methods 0.000 claims abstract description 3
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- -1 chlorine ions Chemical class 0.000 abstract description 4
- 229910052801 chlorine Inorganic materials 0.000 abstract 1
- 239000000460 chlorine Substances 0.000 abstract 1
- 238000011084 recovery Methods 0.000 description 8
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 6
- 230000003647 oxidation Effects 0.000 description 6
- 238000007254 oxidation reaction Methods 0.000 description 6
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 4
- 238000002386 leaching Methods 0.000 description 4
- XCAUINMIESBTBL-UHFFFAOYSA-N lead(ii) sulfide Chemical compound [Pb]=S XCAUINMIESBTBL-UHFFFAOYSA-N 0.000 description 4
- 238000010276 construction Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- WIKSRXFQIZQFEH-UHFFFAOYSA-N [Cu].[Pb] Chemical compound [Cu].[Pb] WIKSRXFQIZQFEH-UHFFFAOYSA-N 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000009854 hydrometallurgy Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C5/00—Electrolytic production, recovery or refining of metal powders or porous metal masses
- C25C5/02—Electrolytic production, recovery or refining of metal powders or porous metal masses from solutions
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C1/00—Electrolytic production, recovery or refining of metals by electrolysis of solutions
- C25C1/18—Electrolytic production, recovery or refining of metals by electrolysis of solutions of lead
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C7/00—Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
Definitions
- the present invention relates to a method for selectively recovering lead from complex sulphidic non-ferrous metal concentrates in an electrolytic cell incorporating at least one anode and one cathode and an electrolyte which contains chloride ions, at a temperature beneath the boiling point of the concentrate-containing electrolyte and at a pH beneath 7, and the sulphur present in the concentrate being converted into an elementary form and at least the major part of the lead content passing into solution and being subsequently precipitated out selectively through a cathodic process.
- DE-C-27 32 817 discloses the selective recovery of lead from complex sulphide material, but requires first total leaching and then selective precipitation of the cations.
- EP-B-0 026 207 proposes a method for selectively recovering lead from complex sulphide concentrates in which physical contact of the particles with the anodes is avoided to the greatest possible extent while, at the same time, limiting the current density to as low a level as possible, preferably between 50 and 100 A/m 2 . It is true that this known method provides a high degree of selectivity, although at the price of low specific lead recovery, i.e. the quantity of lead recovered per unit area of anode, due to the necessary restriction of current density.
- the complex sulphide concentrate charged to the process is collected in the electrolyte to form a suspension.
- the suspension formed in the electrolytic cell is caused to flow onto or closely adjacent to the surfaces of anodes located in the cell.
- surfaces is meant here, and in the following, an electrochemically active surface of the anode.
- the highest possible anodic current density is maintained during the recovery process.
- “highest possible” is meant an anodic current density which will enable the highest possible quantities of lead to be recovered selectively without resulting in troublesome chlorine-gas emission from the cell.
- the anodic current density In order to maintain required selectivity with regard to the lead recovery the anodic current density must not exceed a value at which the concentrate suspension present does not reduce the oxidation agent formed at the anode. Simultaneously a low oxidation potential must be maintained within the suspension in the cell. In this respect there is used in the majority of cases a lowest anodic current density of about 200 A/m 2 .
- the lead leaching and recovery processes are thus carried out in one and the same vessel, electrolytic cell, which is preferably of cylindrical form with electrodes placed radially therein.
- the cell preferably incorporates a diaphragm which separates the anolyte from the catholyte in a known manner.
- the cell is suitably provided with agitating means which lifts the suspension from the bottom of the cell and transports the same upwardly in the centre of said cell. At the upper part of the cell the suspension is caused to flow outwardly from the cell edge and then obliquely down into contact with or along the vertical anode surfaces.
- the agitating means can also be arranged to reverse the direction of flow, in which case the suspension is caused to flow outwardly from the cell edge at the bottom of said cell.
- the flow of suspension into contact with or along, i.e. closely adjacent, the anode surface is controlled in a manner to maintain the rate of flow at a sufficiently high level over all parts of the anode surfaces present in the cell. This will counteract to a large extent the generation of chlorine gas in the cell. The presence of chlorine gas is liable to cause anode corrosion, and is therefore not desirable.
- the maximum current density is dependent on the mass transfer at the anode surface.
- the concentrate is forced into contact with the anode surface, as in the case of the present invention, there is also obtained an effective mass transfer through the high flow of suspension over the anode surfaces.
- the flow is also uniform over the whole of the anode surface.
- the oxidizing agent i.e. the electrolyte
- the oxidizing agent i.e. the electrolyte
- the lead sulphide it is possible, seen as a whole, to supply a maximum amount of oxidizing agent per unit of time to the lead sulphide while retaining the desired degree of selectivity, which is to great advantage.
- the method ensures that in this way lead is leached from the solution in the fastest time possible with respect to the kinetics of the dissolution of the lead sulphide.
- the method can be carried out in any type of electro-winning cell in which a flow of concentrated suspension can be maintained in the immediate vicinity of the anode or anodes.
- an electrolytic cell of cylindrical construction having a first conical bottom in which the electrodes are placed alternately in a star-shaped formation.
- the cell incorporates means for guiding the suspension towards and against the anode surfaces, and also an agitating means placed centrally in the cell.
- the cell is suitably of a construction in which the cathode chambers extend down to the bottom of the cell and through said bottom, beneath which there is arranged a second conical bottom. All lead recovered is collected in this second bottom in the form sponge lead, this lead first forming on the surfaces of the cathode and then falling down gravitationally into the second bottom.
- the sponge lead can be tapped-off through the cell bottom.
- FIG. 1 is a vertical sectional view of the cell and Figure 2 is a top plan view of the cell.
- the cell 1 comprises a vessel 2 having a first conical bottom 3 and a second conical bottom 4 located beneath said first bottom.
- the cell has electrodes arranged radially therein, i.e. in the form of anodes 5 and cathodes 6.
- a diaghragm 7 is placed inbetween the electrodes.
- the cathode chamber 8 is connected directly with the second bottom 4, whereas the anode chamber 9 is connected to the first bottom.
- the electrolyte present in the anode chamber 9 is referred to as anolyte, and the electrolyte present in the cathode chamber as catholyte.
- the agitator 10 causes the suspension of concentrate and anolyte to flow into and up through a conduit 11, as shown by arrows 12,13, and then outwardly and downwardly onto the surfaces 15 of the anodes 5, as shown by the arrows 14.
- the lead ions formed in the anodic reaction precipitate onto the cathodes 6, from which lead metal falls progressively in the form of sponge lead, to be collected in the lowermost conical bottom 4.
- the sponge lead can then be removed through the apex of the conical bottom 4 with the aid of means 16 intended herefor.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Metals (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE8504140 | 1985-05-09 | ||
SE8504140A SE8504140L (sv) | 1985-09-05 | 1985-09-05 | Forfarande for selektiv utvinning av bly fran komplexa sulfidiska icke-jernmetallsliger |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0219473A1 true EP0219473A1 (fr) | 1987-04-22 |
EP0219473B1 EP0219473B1 (fr) | 1990-07-04 |
Family
ID=20361307
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP86850290A Expired - Lifetime EP0219473B1 (fr) | 1985-09-05 | 1986-09-04 | Procédé de récupération sélective du plomb à partir de minearais complexes sulfurés de métaux non ferreux |
Country Status (9)
Country | Link |
---|---|
US (1) | US4734172A (fr) |
EP (1) | EP0219473B1 (fr) |
JP (1) | JPS6260886A (fr) |
AU (1) | AU584450B2 (fr) |
CA (1) | CA1300554C (fr) |
DE (1) | DE3672443D1 (fr) |
FI (1) | FI81614C (fr) |
SE (1) | SE8504140L (fr) |
ZA (1) | ZA866571B (fr) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5635051A (en) * | 1995-08-30 | 1997-06-03 | The Regents Of The University Of California | Intense yet energy-efficient process for electrowinning of zinc in mobile particle beds |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3673061A (en) * | 1971-02-08 | 1972-06-27 | Cyprus Metallurg Process | Process for the recovery of metals from sulfide ores through electrolytic dissociation of the sulfides |
US4204922A (en) * | 1977-12-06 | 1980-05-27 | The Broken Hill Propietary Company Limited | Simultaneous electrodissolution and electrowinning of metals from simple sulphides |
WO1980002164A1 (fr) * | 1979-04-09 | 1980-10-16 | Dextec Metallurg | Production de plomb a partir de minerais et concentres |
EP0061392A1 (fr) * | 1981-03-19 | 1982-09-29 | Centre National De La Recherche Scientifique (Cnrs) | Procédé et dispositif pour l'électrotraitement de matériaux composites pulvérulents |
WO1984002356A1 (fr) * | 1982-12-10 | 1984-06-21 | Dextec Metallurg | Cellule electrolytique pour la recuperation de metaux a partir de materiaux contenant du metal |
-
1985
- 1985-09-05 SE SE8504140A patent/SE8504140L/ unknown
-
1986
- 1986-08-18 CA CA000516135A patent/CA1300554C/fr not_active Expired - Fee Related
- 1986-08-18 AU AU61525/86A patent/AU584450B2/en not_active Ceased
- 1986-08-19 FI FI863351A patent/FI81614C/fi not_active IP Right Cessation
- 1986-08-29 ZA ZA866571A patent/ZA866571B/xx unknown
- 1986-09-01 JP JP61205738A patent/JPS6260886A/ja active Pending
- 1986-09-04 EP EP86850290A patent/EP0219473B1/fr not_active Expired - Lifetime
- 1986-09-04 DE DE8686850290T patent/DE3672443D1/de not_active Expired - Lifetime
- 1986-09-05 US US06/904,010 patent/US4734172A/en not_active Expired - Fee Related
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3673061A (en) * | 1971-02-08 | 1972-06-27 | Cyprus Metallurg Process | Process for the recovery of metals from sulfide ores through electrolytic dissociation of the sulfides |
US4204922A (en) * | 1977-12-06 | 1980-05-27 | The Broken Hill Propietary Company Limited | Simultaneous electrodissolution and electrowinning of metals from simple sulphides |
WO1980002164A1 (fr) * | 1979-04-09 | 1980-10-16 | Dextec Metallurg | Production de plomb a partir de minerais et concentres |
EP0061392A1 (fr) * | 1981-03-19 | 1982-09-29 | Centre National De La Recherche Scientifique (Cnrs) | Procédé et dispositif pour l'électrotraitement de matériaux composites pulvérulents |
WO1984002356A1 (fr) * | 1982-12-10 | 1984-06-21 | Dextec Metallurg | Cellule electrolytique pour la recuperation de metaux a partir de materiaux contenant du metal |
Also Published As
Publication number | Publication date |
---|---|
EP0219473B1 (fr) | 1990-07-04 |
FI81614B (fi) | 1990-07-31 |
AU584450B2 (en) | 1989-05-25 |
JPS6260886A (ja) | 1987-03-17 |
AU6152586A (en) | 1987-03-12 |
FI863351A (fi) | 1987-03-06 |
CA1300554C (fr) | 1992-05-12 |
SE8504140D0 (sv) | 1985-09-05 |
FI81614C (fi) | 1990-11-12 |
ZA866571B (en) | 1987-05-27 |
FI863351A0 (fi) | 1986-08-19 |
DE3672443D1 (de) | 1990-08-09 |
US4734172A (en) | 1988-03-29 |
SE8504140L (sv) | 1987-03-06 |
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